Experimental study of liquid/dense-gas pipe flow

被引:2
作者
Quintino, Andre Mendes [1 ,3 ]
da Fonseca Junior, Roberto [2 ]
Rodriguez, Oscar Mauricio Hernandez [3 ]
机构
[1] Norwegian Univ Sci & Technol, Dept Geosci & Petr, SP Andersens Veg 15, N-7031 Trondheim, Norway
[2] Petrobras SA, CENPES PDIEP EE, Ave Horacio Macedo 950, BR-21941915 Rio de Janeiro, Brazil
[3] Univ Sao Paulo, Sao Carlos Sch Engn, Mech Engn Dept, Ind Multiphase Flow Laboratory LEMI, Ave Joao Dagnone,1100 Santa Angelina, BR-135643120 Sao Carlos, SP, Brazil
来源
GEOENERGY SCIENCE AND ENGINEERING | 2023年 / 230卷
关键词
Two-phase flow; Experimental; Dense gas; Flow patterns; Holdup; Pressure gradient; 2-PHASE FLOW; PREDICTING FLOW; PATTERN; TRANSITIONS; MODEL;
D O I
10.1016/j.geoen.2023.212179
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
The pre-salt reservoirs play a significant role in the current Brazilian ultradeep water offshore scenario. Their importance is expected to increase soon. The fluids are transported through horizontal, inclined, and vertical wells of several kilometers, and due to the environmental conditions at the reservoir, dense-gas/liquid flow occurs in the pipelines. However, the literature lacks experimental data for gas-liquid flow with densities of the same order of magnitude, which affects the mechanistic model's accuracy for flow patterns, pressure gradients, and holdup predictions. To improve the understanding of that specific two-phase flow, an experimental apparatus was built, and an experimental study was carried out using sulfur hexafluoride (100 kg/m3) and mineral oil (850 kg/m3) at medium pressures. A density ratio lower than 10 was obtained for steady-state horizontal flow in a 50.8-mm-i.d. stainless-steel pipe, and flow patterns, pressure gradient, and holdup were measured. The experimental results show the effect of the low-density ratio on the stratified to non-stratified flow-pattern transition and the occurrence of the dual-continuous flow pattern at high mixture superficial velocity. Moreover, the pressure gradient and holdup data were compared with the results of a commercial multiphase flow simulator, showing good agreement.
引用
收藏
页数:13
相关论文
共 27 条
[1]   Experimental and modeling studies for gas-liquid two-phase flow at high pressure conditions [J].
Abduvayt, P ;
Arihara, N ;
Manabe, R ;
Ikeda, K .
JOURNAL OF THE JAPAN PETROLEUM INSTITUTE, 2003, 46 (02) :111-125
[2]  
Almabrok A.A., 2013, Gas-Liquid two-phase flow in up and down vertical pipes
[3]  
[Anonymous], 2005, BHR INT C MULTIPHASE
[4]   A UNIFIED MODEL FOR PREDICTING FLOW-PATTERN TRANSITIONS FOR THE WHOLE RANGE OF PIPE INCLINATIONS [J].
BARNEA, D .
INTERNATIONAL JOURNAL OF MULTIPHASE FLOW, 1987, 13 (01) :1-12
[5]   FLOW PATTERN TRANSITION FOR GAS-LIQUID FLOW IN HORIZONTAL AND INCLINED PIPES - COMPARISON OF EXPERIMENTAL-DATA WITH THEORY [J].
BARNEA, D ;
SHOHAM, O ;
TAITEL, Y ;
DUKLER, AE .
INTERNATIONAL JOURNAL OF MULTIPHASE FLOW, 1980, 6 (03) :217-225
[6]  
Belt R., 2011, 15th Int. Conf. Multiph. Prod. Technol, P413
[7]   ONSET OF SLUGGING IN HORIZONTAL GAS-LIQUID PIPE-FLOW [J].
BENDIKSEN, K ;
ESPEDAL, M .
INTERNATIONAL JOURNAL OF MULTIPHASE FLOW, 1992, 18 (02) :237-247
[8]  
Bendiksen K.H., 1991, DYNAMIC 2 FLUID MODE
[9]  
Bigdeli A., 2023, EFFECT LIQUID LIQUID
[10]  
Brito A., 2014, SPE LATIN AM CARIBBE, P178